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Applied energy v.212, 2018년, pp.1191 - 1202   SCI SCIE
본 등재정보는 저널의 등재정보를 참고하여 보여주는 베타서비스로 정확한 논문의 등재여부는 등재기관에 확인하시기 바랍니다.

Techno-economic analysis of biogas upgrading via amine scrubber, carbon capture and ex-situ methanation

Vo, Truc T.Q. (MaREI Centre for Marine and Renewable Energy, Environmental Research Institute, University College Cork (UCC), Cork, Ireland ) ; Wall, David M. (MaREI Centre for Marine and Renewable Energy, Environmental Research Institute, University College Cork (UCC), Cork, Ireland ) ; Ring, Denis (School of Engineering, University College Cork, Ireland ) ; Rajendran, Karthik (MaREI Centre for Marine and Renewable Energy, Environmental Research Institute, University College Cork (UCC), Cork, Ireland ) ; Murphy, Jerry D. (MaREI Centre for Marine and Renewable Energy, Environmental Research Institute, University College Cork (UCC), Cork, Ireland ) ;
  • 초록  

    Abstract Biogas upgraded to biomethane can provide a renewable gaseous transport fuel and is one of the proposed solutions in meeting the renewable energy supply in transport targets set under the EU Renewable Energy Directive. The upgrading process for biogas involves the removal of CO 2 . Amine scrubbing is one traditional method of upgrading that is applied due to its low methane slippage and its capability to provide a high purity renewable methane product. However, new technologies such as power to gas (P2G) can also upgrade biogas through biological methanation by combining the CO 2 in biogas with H 2 to produce renewable methane. The H 2 for P2G can be produced through electrolysis of renewable electricity. Through simulation software – SuperPro Designer, the economics of different pathways for upgrading biogas from a grass silage and slurry fed digester are analysed and compared in this paper. Three scenarios were investigated: biogas upgrading through amine scrubbing (scenario 1); biogas upgrading through amine scrubbing with CO 2 directed to ex-situ biological methanation (scenario 2) and biogas upgrading through ex-situ biological methanation only (scenario 3). The results show that at a net present value of zero, the minimum selling price (MSP) per m 3 of renewable methane for scenario 1, 2 and 3 is €0.76; €1.50 and €1.43, respectively (with an electricity price to produce H 2 of €0.10/kWh and a grass silage production cost of €27/t). The electricity price has a significant effect on the cost of renewable methane in both scenarios 2 and 3. The MSP reduces to €1.09 and €1.00 per m 3 of renewable methane, respectively for scenarios 2 and 3, if the electricity price is reduced to €0.05/kWh. Since the renewable methane MSP from scenario 2 is higher than scenario 3, it is suggested that direct biogas injection to the methanation reactor is financially more attractive than capturing CO 2 from biogas and feeding it to the methanation step. The MSP of renewable methane from both scenarios 2 and 3 are significantly higher than that of scenario 1. However, when considering climate change mitigation, balancing of the electricity network and storage of surplus electricity, utilising P2G can offset some of these costs. The cost of H 2 is a significant factor in determining the cost of renewable methane. Highlights Three biogas upgrading scenarios were simulated in SuperPro Designer. Scenario 1 modelled digestion of grass and silage with amine scrubbing. Scenario 2 doubled methane output through reaction of CO 2 from scrubbing with H 2. Scenario 3 employed biomethanation reacting biogas with H 2 removing amine scrubbing. Costs of CH 4 from scenario 1, 2 and 3 per m 3 are €0.76, €1.50 and €1.43. Graphical abstract [DISPLAY OMISSION]


  • 주제어

    CO2 capture .   Process simulation .   Amine scrubber .   Methanation .   Biological power to gas .   Economic analysis.  

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